pes_ornek
TRANSCRIPT
-
7/30/2019 PES_ornek
1/9
Properties of Linear Poly(Lactic Acid)/PolyethyleneGlycol Blends
K. Sungsanit, N. Kao, S.N. BhattacharyaSchool of Civil, Environmental and Chemical Engineering, Rheology and Materials Processing Centre,
RMIT University, Melbourne, Victoria 3001, Australia
Poly(lactic acid) (PLA) has great potentials to be proc-essed into films for packaging applications. However,film production is difficult to carry out due to the brit-tleness and low melt strength of PLA. In this investiga-tion, linear PLA (L-PLA) was plasticized with poly(ethyl-ene glycol) (PEG) having MW of 1000 g mol21 in variousPEG concentrations (0, 5, 10, 15, and 20 wt%). In rela-tion to plasticizer content, the impact resistance and
crystallinity of L-PLA was increased, whereas adecrease in glass transition temperature and lowerstiffness was observed. Nevertheless, the phase sepa-ration has been found in samples which contained PEGgreater than 10 wt%. The dynamic and shear rheologi-cal studies showed that the plasticized PLA possessedlower viscosity and more pronounced elastic proper-ties than that of pure PLA. Both storage and loss mod-uli decreased with PEG loading at all frequencies whilestorage modulus exhibited weak frequency depend-ence with increasing PEG content. POLYM. ENG. SCI.,52:108116, 2012. 2011 Society of Plastics Engineers
INTRODUCTION
Poly(lactic acid) (PLA) is produced from renewable
resources that has become a useful material, especially in
packaging applications due to its good clarity, high
strength, and moderate barrier properties. PLA resins have
mostly been used for biomedical applications such as drug
delivery systems and packaging applications such as films
and food containers [1]. Some of the environmental bene-
fits of PLA and opportunities for the future are presented
by Henton et al. [2]. These include PLA requiring less
energy to produce as well as reduced green house gas
production. Generally, commercial grades PLA are
copolymers of poly(L-lactic acid)(PLLA) and poly(D,L-lac-
tic acid) (PDLLA), which are produced from L-lactides
and D,L-lactides, respectively. PLLA is a semicrystalline
polymer whereas PDLLA is an amorphous polymer.
PLAs use in film packaging applications is highly de-
sirable due to its environmentally friendly nature. How-
ever, this requires film extrusion of PLA to be performed,
which is difficult to process due to the brittleness and low
melt strength of PLA. The rheological and mechanical
properties of PLA may be enhanced by blending it with a
plasticizer or with a second polymer. For instance, it could
be blended with other polymers such as linear low density
polyethylene [3], poly(vinyl acetate) [4] and polyethylene
glycol (PEG) [5, 6]. Possible plasticizers for PLA include
oligomeric lactic acid, lactide and low molecular weight
esters such as citrates [7]. These blends have been shown to
improve the flexibility of PLA. However, some of the
above-mentioned polymers are not biodegradable; hence,
they could not be considered as a possible blend with PLA
in this investigation. In consumer goods packaging applica-
tions, only nontoxic substances approved for food contact
can be considered as plasticizing agents. The selection of a
plasticizer to be used in a specific PLA composition
requires the consideration of many criteria: compatibility,
low volatility, resistance to migration, extraction during
service life, lack of toxicity, etc. [8].
Low molecular weight PEG is the most suitable mate-
rial to be classed as an impact modifier for PLA due to
its miscibility, biodegradability, and food contactable
applications [6, 911]. Jacobsen et al. [9] investigated the
plasticized PLA, with 2.510 wt% of PEG (MW 1.5 310
3) by melt blending. They found that the addition of
PEG to PLA led to a decrease of both tensile strength and
elasticity modulus but an increase of percentage elonga-
tion at break. Adding 10 wt% PEG resulted in an
enhanced impact resistance of more than five times that
of a pure PLA. Kulinski et al. [11] investigated the blend-
ing of semicrystalline and amorphous PLA with 5 and 10
wt% of PEG. They reported that at 10 wt%, an amor-
phous plasticized PLA could be deformed to about 550%
while a semicrystalline PLA exhibited nonuniform plasti-
cization of the amorphous phase and showed less ability
to the plastic deformation. Sheth et al. [5] have found that
PLA/PEG blends varied from completely miscible to par-
tially miscible, depending on the PEG concentration.
Below 50 wt% PEG content, the blends achieved the
higher elongations and lower modulus values. Above 50
wt% PEG content, the blend morphology was driven by
K. Sungsanit is currently at Rajamangala University of Technology
Thanyaburi, Pathumthani, Thailand.
Correspondence to: K. Sungsanit; e-mail: [email protected]
DOI 10.1002/pen.22052
Published online in Wiley Online Library (wileyonlinelibrary.com).
VVC 2011 Society of Plastics Engineers
POLYMER ENGINEERING AND SCIENCE-2012
-
7/30/2019 PES_ornek
2/9
the increasing crystallinity of PEG, resulting in an
increase in modulus and a corresponding decrease in elon-
gation at break. Recent studies [6, 10] of PLA plasticized
with PEG in various contents have shown a limit of mis-
cibility of polymer blends. The PLA blended to PEGsbecame very brittle as a function of plasticizer content
and molecular weight. The plasticizing efficiency
increased with decreasing molecular weight of PEG. In
contrast, at the same molecular weight of PEG, material
became brittle at higher content because of a lack ofcohesion between the separate phases.
This article investigates the effect of plasticization on
the properties of L-PLA/PEG blends at various PEG con-
tents. Differential scanning calorimetry (DSC) was carried
out in a wide range of temperatures in order to evaluate
crystallization and melting behavior of the blends. Fur-
thermore, impact and tensile properties were investigated
to evaluate the outcome of PLA plasticization with PEGfor film applications. Surprisingly, there is very little liter-
ature examining the plasticizing effects of PEG on the
rheological properties in terms of steady shear and
dynamic measurements of PLA/PEG blends which play
important roles in polymer processing. Thus, the melt rhe-
ology of pure L-PLA and plasticized L-PLA was con-
ducted in this study and the results are presented below.
EXPERIMENTAL
Materials
The poly(lactic acid) (4032D-grade) from NatureWorksproduced by Cargill Dow LLC, used in this study, com-
prised of 2% D-LA content. Polyethylene glycol (molecular
weight 1000 g/mol), a food-contact approved grade from
Sigma-Aldrich, was chosen as a plasticizer for the L-PLA.
The materials used and their properties are listed in Table 1.
Blending Preparation
L-PLA pellets were dried in an oven under vacuum at
508C overnight (1215 h) prior to blending. Drying was
necessary to minimize the hydrolytic degradation of the
polymers during melt processing in the extruder. L-PLA
and PEG were melt-blended using a Brabender twin-
screw extruder in the ratio of 100/0, 95/5, 90/10, 85/15,
and 80/20 where the first and second number represent L-
PLA and PEG by weight percentage, respectively. For
better comparison, the pure L-PLA sample was also proc-
essed in the same twin screw extruder and processing
conditions to ensure identical thermal history with thoseof L-PLA/PEG blends. Dry-mixing of each polymer was
first carried out in a zip-lock bag before blending. The
twin screw extruder had a screw diameter of 17.8 mm
and an L/D ratio of 40. The extruder had three controlled
temperature zones which were set from 1808C (next to
the feeding segment), 1908C (compression zone) and
2008C (metering zone). The screw speed was maintained
at 30 rpm for all runs. Subsequently, plasticized L-PLA
pellets were dried again under vacuum at 508C overnight
prior to sample preparation by injection and compression
molding.
Differential Scanning Calorimetry
Differential scanning calorimetry (DSC) was carried
out with a DSC TA Instrument 2920. The samples were
preliminarily heated to 473 K to discard any anterior ther-
mal history and held at that temperature for 5 min. It was
then cooled to 253 K at a rate of 10 K min21
and kept at
253 K for 5 min before a second heating scan from 253
to 473 K at 10 K min21
scan rate was carried out. During
the second heating scan the glass transition, cold crystalli-
zation and melting temperature of the material could be
determined; whilst the crystallization temperature was
determined from the cooling scan. The degree of crystal-linity of all samples were calculated by
Crystallinity % DHm DHcc=UPLA
93:6 100: (1)
Most commonly, an enthalpy of fusion of 93.6 J g21
is
used for a 100% crystalline PLLA or PDLA homopoly-
mers [12], where DHm is the measured heat of fusion and
DHcc is the heat of cold crystallization. This value is used
throughout the PLA literature. FPLA is the PLA content in
the component.
Mechanical Characterization
Tensile measurements were carried out to determine
the tensile strength, tensile modulus and % strain at break
using the Instron 4467 Universal testing machine at room
temperature. The testing was carried out at a rate of 5
mm min21 according to ASTM D638 on standard Type I
dog-bone shaped samples with sample thickness of 4.1
mm.
The impact resistance was determined for each mate-
rial with 10 samples, which were tested under the temper-
TABLE 1. Properties of PLA and plasticizer used in this study.
Materials
Mw(g/mol)
Tm(K)c
Tg(K)c
Chemical
formula
Linear poly
(lactic acid)
(L-PLA)
155,000a 442 334
Poly(ethylene
glycol) (PEG)
1,000b 313 203
aDetermined by Gel Permeation Chromatography (GPC) versus
polystyrene standards.b As stated by the manufacturer.c
Determined by Differential Scanning Calorimetry (DSC).
DOI 10.1002/pen POLYMER ENGINEERING AND SCIENCE-2012 109
-
7/30/2019 PES_ornek
3/9
ature like the tensile test and following the ASTM stand-
ard specification ASTM D256, the so-called izod method,
with a Davenport impact tester. The samples were
notched and a pendulum hammer of 1.36 J was used.
Both tensile and impact samples were injection molded
and were dried in the vacuum oven at 508C over night
prior to testing.
Rheological Characterization
The rheological properties of L-PLA with various PEG
contents were measured using an Advanced RheometricExpansion System (ARES) fitted with a 25 mm parallel
plate geometry. Tests were performed at 1808C under a
nitrogen atmosphere to avoid any degradation. Sample
disks for the rheometer were compression molded at
2008C into 25 mm diameter discs $3.2 mm thick andwere again dried in the vacuum oven overnight at 508C
prior to testing.
Dynamic strain sweep tests were carried out to confirm
the linearity of the viscoelastic region up to 100% strain
at 10 rad s21 frequency. Frequency sweeps were carried
out to determine the dynamic moduli and complex viscos-
ity over a frequency range of 0.1100 rad s21
at 10%
strain. All tests were started when the temperature had
stabilized after loading the sample into the rheometer.
Steady shear measurements were performed over a shear
rate range of 0.0110 s21
.
Fractured Surface CharacterizationThe fractured surfaces of all materials were observed
by Environmental Scanning Electron Microscopy
(ESEM), using a Philips XL-20 SEM at an accelerating
voltage of 30 kV. All of the samples were fractured speci-
mens after impact tests. The fractured surface was then
coated with a thin layer of gold prior to observation.
RESULTS AND DISCUSSION
Thermal Properties
The results obtained from differential scanning calo-
rimetry of the pure L-PLA (unprocessed and 0 wt% PEG)
and plasticized L-PLA are shown in Fig. 1 and important
numerical values are summarized in Table 2.
Table 2 summarizes the glass transition temperature
(Tg) of plasticized L-PLA as well as crystallization and
melting temperatures (Tc and Tm). Pure PLA showed a
sharp Tg and its magnitude decreased gradually with
increasing PEG concentration. A minor decrease in the
melting temperature (Tm) of 3 to 4 K was also observed,
indicating that the melting temperature of L-PLA was not
greatly affected by the addition of PEG. According to
DSC thermograms (Fig. 1a), the crystallization tempera-ture (Tc) seemed to be increased with increasing PEG
content. This was due to the presence of the plasticizer,
which facilitated the crystallization process of PLA. As
noted previously, the increased molecular mobility
increased the rate of crystallization, which allowed L-
PLA to crystallize to a higher degree during cooling [1]
and allowing the crystallization of L-PLA to occur at a
higher temperature (i.e., with less sub-cooling). This is in
accordance with the crystallization behavior of PLA as
reported by Miyata et al. [13]. However, there was an
irregular characteristic of Tc which showed sudden
decrease from 369 K to 363 K in the presence of a small
amount of plasticizer at 5 wt% PEG. It is presumed thatduring the non-isothermal crystallization temperature from
473 K to 253 K, L-PLA initially crystallized before the
formation of PEG crystals at temperature range between
373 K and 363 K. On the other hand, PEG crystallized
following the formation of L-PLA crystals between 303 K
and 293 K (determined by DSC). Consequently, during
the formation of L-PLA crystals some molecules of PEG
probably could be trapped in the intra-spherulitic region
of L-PLA and led to hindering the crystallization of L-
PLA. Nevertheless, addition more wt% of PEG enhances
FIG. 1. Effect of PEG concentration on crystallization and melting of
L-PLA/PEG blends: (a) cooling thermograms obtained with a cooling
rate of 10 K min21
; (b) subsequent heating thermograms obtained with a
heating rate of 10 K min21
.
110 POLYMER ENGINEERING AND SCIENCE-2012 DOI 10.1002/pen
-
7/30/2019 PES_ornek
4/9
degree of the crystallization rate of L-PLA as seen in
Table 2.
In contrast, as seen in Fig. 1b for 0 wt% PEG, the Tgwas observed to be approximately 335 K. At 5 wt% PEG
the Tg decreased to approximately 319 K and down to
306 K when up to 15 wt% PEG was added. However, for
blend compositions having higher concentration of PEG,
there was no change in the Tg of L-PLA/PEG blends.
Moreover, the plasticized L-PLA showed crystallinity
between 36% and 44% for all the four different polyethyl-
ene glycol contents examined. Fig. 1b shows that the cold
crystallization temperature (Tcc) of L-PLA decreased in
the presence of the plasticizer. For the un-processed L-
PLA, the thermograms did not show the cold crystalliza-
tion peak since the material did not go through the ther-
mal process. While the processed L-PLA without PEG (0
wt % of PEG) showed the cold crystallization temperature
of 373 K and suddenly decreased to 263 K for the L-
PLA/PEG sample containing 10 wt% of PEG. For sam-
ples containing higher PEG content, cold crystallization
was no longer visible. In the present blends, comparedwith that of pure L-PLA, the depression of Tg and the sig-
nificant decrease in Tcc indicated that polyethylene glycol
was compatible and effective with L-PLA. It clearly
appeared that the decreasing of Tcc and Tg of L-PLA due
to enhanced chain mobility as the plasticizer level
increased. Pillin et al. [6] has also reported this behavior.
It was also interesting to see that the small melting and
crystallization peaks of PEG were seen for L-PLA/PEG
blends containing 15 and 20 wt% plasticizer concentration
(in the circle of Fig. 1a and b) instead of the observation
of the glass transition of blends. It is possible that there
was the phase-separation of pure PEG in this blend (com-
pared with melting temperature of PEG 1000 in Table 1).It is obvious that to facilitate the plastic deformation of
semicrystalline polymer, with glassy amorphous phase,
the plasticization of the latter and sufficient decrease of
Tg are required. However, crystallization while increasing
the average plasticizer content in the amorphous phase
may also induce a rejection of plasticizer from growing
spherulites and its accumulation at interspherulitic boun-
daries [14]. In the L-PLA/PEG blends investigated in this
work, segregation of a pure PEG phase always occurred
at plasticizer content higher than 10 wt%. From the DSC
analysis, it could be concluded that the PEG plasticizer
has ability to increase ductility of L-PLA by increasing
the mobility of L-PLA molecules.
Tensile Properties
The objective of plasticization is to improve the ductil-
ity while maintaining the blends strength and stiffness.
Results of tensile experiments are shown in Figs. 24.
When L-PLA sample was stretched without PEG, the ten-
sile strength, tensile modulus and % tensile strain at break
were 49 MPa, 4.3 GPa, and 1.3%, respectively. For plasti-
cized L-PLA at 5 wt% and 10 wt% PEG, the tensile
strength was 56 and 51, MPa, respectively. The higher
tensile strength values were due to the higher crystallinity
content than that of the L-PLA with 0 wt% of PEG
(whose tensile strength was only 49 MPa). Tensile
strength of the L-PLA/PEG blends gradually decreased to
29 and 22 MPa, when higher concentrations (15 and 20
wt %, respectively) of PEG were used (see Fig. 2). From
thermal characterization, it was clear that phase separationof L-PLA/PEG blends in this investigation could be
observed at PEG concentration of more than 10 wt%.
Moreover, from Fig. 3, a gradual decrease in the tensile
TABLE 2. Results from DSC for the L-PLA/PEG Blends.
PEG content (wt%)
Cooling Subsequent heating
Tc (K) DH (J g21) Tg (K) Tcc (K) DH (J g
21) Tm (K) DH (J g21) Xc (%)
Un-processed PLA 334 442 12 13
0 369 12 335 373 12 444 38 27
5 363 13 319 365 7 443 39 36
10 368 21 311 363 1 443 34 40
15 371 30 306 441 30 3920 378 30 306 440 33 44
All data are the average data.
FIG. 2. Effect of PEG concentration on tensile strength of L-PLA/PEG
blends.
DOI 10.1002/pen POLYMER ENGINEERING AND SCIENCE-2012 111
-
7/30/2019 PES_ornek
5/9
modulus from 4.3 to 1.9 GPa was observed as the concen-
tration of PEG increased from 0 to 20 wt% in the L-PLA/
PEG blends.
In the meantime, the tensile strain at break (see Fig. 4)
increased from 1.5% to 15% with increasing PEG content
of 0 wt% and 20 wt% PEG, respectively.
Impact Properties
The impact resistance properties of L-PLA/PEG blends
are shown in Fig. 5. Clearly, it could be seen that the
presence of PEG as a plasticizer in L-PLA marginally
increases the toughness of L-PLA. For L-PLA/PEG bland
(0 wt% PEG), the average value was 13.3 kJ/m2 but the
data increased dramatically to 15.4 and 14.9 kJ m22 for
L-PLA/PEG samples containing 5 and 10 wt% PEG,
respectively. As expected, the increase in impact strength
of L-PLA was observed when plasticized with PEG
because the plasticizer interacted with the polymer chainsdistributing itself uniformly within the polymer, hence
creating additional free volume. However, the decrease in
impact strength was also observed when PEG concentra-
tion reached 15 and 20 wt% due to separation of PLA
and PEG phases as seen from thermal characterization.
This indicated that the blends were ductile at less than 10
wt% plasticizer content and were brittle at greater than 15
wt% plasticizer content.
It should be noted that it is important to have informa-
tion about the impact resistance behavior at other defor-
mation rates as well. Because of some differences
between tensile and impact deformation rates, it has beenfound in this investigation that blends with high elonga-
tion at break were characterized by relatively weak
impact values. Therefore, it is important to note that for
plasticized blends with high content of plasticizer (PEG)
a decrease in impact strength has been reported. Jacobsen
and Fritz [9] attributed this to a disturbance created by
the plasticizer composition into PLA matrix.
Surprisingly, the abrupt change of all mechanical prop-
erties occurred regularly in L-PLA/PEG blends whose
PEG concentrations were greater than 10 wt%. For higher
PEG concentrations, the material became brittle due to an
occurrence of phase separation at the saturated points of
PEG content. This could result only from a phase separa-tion in the amorphous phase leading to the formation of a
plasticizer rich phase and depleting the PLA of plasti-
cizer. SEM studies of fractured surfaces of impact bar as
shown in Fig. 6 illustrated some emptied voids and round
white particles in L-PLA/PEG blends (15 and 20 wt% of
PEG) where PEG accumulated during phase separation.
The fractured surfaces represented the dispersion of PEG
phases in L-PLA matrix uniformly and the size of the
PEG domains was of sub-micrometer order. Additionally,
the rich PEG phase and smooth plane could be seen moreFIG. 4. Effect of PEG concentration on % strain at break of L-PLA/
PEG blends.
FIG. 5. Effect of PEG concentration on the impact strength of L-PLA/
PEG blends.
FIG. 3. Effect of PEG concentration on tensile modulus of L-PLA/PEG
blends.
112 POLYMER ENGINEERING AND SCIENCE-2012 DOI 10.1002/pen
-
7/30/2019 PES_ornek
6/9
clearly at the fractured surface of 20 wt% PEG, indicating
the phase separation and brittle failure of L-PLA/PEG
blends. Furthermore, the phase separation in the amor-
phous phase was already reflected in additional low tem-
perature glass transitions of the blends and in melting
peaks of PEG crystals in L-PLA/PEG blends evidenced
by the DSC measurements as shown in Fig. 1b. Upon
phase separation the PEG plasticizer accumulated in dis-
tinct pools.
Fractured Surface Analysis by SEM
The SEM micrographs revealed rather brittle fracture
of L-PLA/PEG blend (0 wt% PEG) with little amount of
plastic deformation with significant lateral contraction of
the test bar and many striated ridges as shown in Fig. 6
(15003 magnification). The lateral contraction and ridgesare the morphological manifestation of the fact that shear-
yielding had occurred during the impact test, resulting in
a ductile break. Figure 6 SEM micrographs of the impact-
fractured surfaces show more evidences of ductile frac-
tures as more and longer fibrils can be observed from the
surfaces with the increase in PEG content. Ductile fibril
formations were observed on the impact surfaces as
shown in Fig. 6ac. In contrast, these fibrils were
observed barely in sample without PEG at $5 lm lengthbetween the striated ridges and there was no longer fibril
on fractured surfaces of PLA/PEG blends (15 and 20 wt%
PEG). It has been reported [15] that this kind of fibril for-
mation appeared to be related to the increase of the tem-
perature in the crack-tip region above the glass transition
temperature due to heat generation at high strain-rate. The
Fig. 6b and c. shows the surface of the blend at 510
wt% PEG. There were more fibrils and roughness on the
surface compared with sample without PEG. This proved
that the PEG was equally dispersed into L-PLA matrix,which made the sample slightly more ductile. When PEG
content was above 10 wt%, the small cavities and white
round shapes of PEG were observed in Fig. 6d and e. The
white round shapes showed broad distribution at 15 wt%
PEG content. The distribution of the white round shapes
increased (as shown in Fig. 6e) with increasing PEG con-
tent (20 wt%). In addition, the sample containing 20 wt%
PEG content also showed a smooth fractured surface indi-
cating brittle fractured areas with considerable voids of
submicron size are clearly observed, which was probably
caused by the accumulation of PEG during phase separa-
tion.
Rheological Properties
To fully understand the processing properties of plasti-
cized L-PLA blends, a detailed investigation of the rheo-
logical behavior of these L-PLA/PEG blends with varying
PEG concentration was necessary.
Figure 7 presents the dynamic viscosity properties on
frequency at various PEG concentrations at 1808C. The
unprocessed L-PLA data were obtained from dynamic fre-
quency sweep measurement carried out on the nonex-
truded pellets. It exhibited a clear Newtonian Plateau atlow oscillation frequency with a zero-shear rate viscosity
around 1000 Pa s and seemed to be shear thinning behav-
ior at high oscillation frequency. On the other hand, the
processed L-PLA also exhibited a non-Newtonian behav-
ior, but with a much lower zero-shear rate viscosity value
(around 840 Pa s). All L-PLA/PEG blends of varying
FIG. 6. SEM micrographs (15003) of the fractured surfaces of the L-
PLA/PEG blends with (a) 0, (b) 5, (c) 10, (d) 15, and (e) 20 wt% PEG.
FIG. 7. Dependence of dynamic viscosity on frequency at various PEG
concentrations at 1808C.
DOI 10.1002/pen POLYMER ENGINEERING AND SCIENCE-2012 113
-
7/30/2019 PES_ornek
7/9
PEG concentrations exhibited a more pronounced Newto-
nian response with an extended Newtonian plateau com-
pared with unprocessed PLA and also showed the
decreasing zero-shear viscosity values as the PEG concen-
tration increased. This was the effect of more disentangle-ment of PLA chain due to increased segmental mobility
of PLA chains.
Additionally, it could be noticed from Fig. 7 that by
blending in the twin screw extruder the polymer was
exposed to excessively high shear strains resulting in a
greater degradation of the PLA. Moreover, the degrada-
tion in PLA during processing in the presence of plasti-
cizers with ester groups could also be due to potential
transesterification reactions leading to a decrease of PLA
molecular weights [16] which resulted in a decrease in
PLA viscosity.
The corresponding storage and loss moduli for theseblends are shown in Figs. 8 and 9, respectively. As
expected, the moduli of L-PLA decreased with increasing
plasticizer loading at all frequencies. Unprocessed L-PLA
and plasticized L-PLA (0-20 wt% of PEG) exhibited the
rheological behavior of a typical polymer melt as charac-
terized by a storage modulus (G0, Fig. 8) smaller than the
loss modulus (G00, Fig. 9). Both the G0 and G00 decreased
with increasing PEG concentration. However, at low-fre-
quency G0 of all blends presented lower frequency de-
pendency. Only at high frequencies, all samples approxi-
mately showed a common storage modulus. Such a non-
terminal behavior, sometime occurs at a medium
frequency region, as has been observed on many polymerblends and is accepted to be attributed to the change of
the shape of the discrete phase in the polymer matrix dur-
ing the oscillatory shear deformation, namely shape relax-
ation [17, 18].
In this investigation, at medium to low frequency
region the storage modulus exhibited weak frequency de-
pendency with increasing PEG content, such that there
were gradual changes of behavior from liquid-like (G0(x)
! x2
) to solid-like with increasing PEG content. At
frequency less than 1 rad s21
, the frequency dependent
transition of the blend with PEG concentration less than
10 wt% could be observed. On the other hand, the
frequency dependent transition of L-PLA/PEG blends at
PEG concentration higher than 10 wt% showed a medium
frequency dependent region between 1 and 10 rad s21. It
could be concluded that at higher PEG concentration the
G0 curves exhibited a plateau distinctly at the low fre-
quencies as the blends seemed to be a solid like behavior.
However it illustrated the discrete phase as well in thematrix if the plasticizer saturation point was reached. As
seen in Fig. 8, the slope of log G0 vs. log x for the unpro-
cessed L-PLA was close to 2, similar to the thermo-rheo-
logically simple polymer in the terminal regime. In con-
trast, the slopes of the storage moduli, in the terminal
region of low frequencies (0.11 rad s21), for L-PLA/
PEG blends were much smaller than 1 (in fact close to
0.5), especially for the blends containing 15 wt% and 20
wt% of PEG. Zheng et al. and Du et al., [19, 20] reported
that the experimental values of the slope for G0 obtained
from other phase separated or degraded polymer blends
varied between 0.5 and 1. Therefore, the small values of
these exponents suggested that the high concentration of
PEG may have contributed to the phase separation in
these blends as verified in the thermal and mechanical
characterization.
In addition, the use of a plasticizer reduces the inter-
molecular force and increases the mobility of the poly-
meric chains, thereby improving the flexibility and the
extensibility of the lasticized polymer [21].
The dependences of the dynamic loss moduli of L-PLA/
PEG blends on frequency (see Fig. 9) indicated that the
blends with higher PEG content had lower G00 values than
that of unprocessed L-PLA over the frequency range cov-
ered. This was due to the fact that G00
represented the vis-cous behavior (i.e., the amount of energy dissipated), and
the addition of PEG to the L-PLA produced a material with
the lowest energy dissipation. From the view of miscibility
of blends, the interaction between blends decreased to a
certain extent at higher PEG content. Hence decreasing in
FIG. 8. Dependence of storage modulus (G0) on frequency at various
PEG concentration in L-PLA/PEG blends at 1808C.
FIG. 9. Dependence of loss modulus (G00) on frequency at various PEG
concentration in L- PLA/PEG blends at 1808C.
114 POLYMER ENGINEERING AND SCIENCE-2012 DOI 10.1002/pen
-
7/30/2019 PES_ornek
8/9
amount of energy dissipated of blends melting with all load
resulted in the decreased loss modulus [22].
Figure 10 shows the steady shear viscosity of L-PLA/
PEG blends at various PEG content. As expected both
unplasticized and plasticized L-PLA melts behaved as
typical non-Newtonian fluids. At all shear rates, the shear
viscosities of L-PLA/PEG blends were lower than those
of pure L-PLA melt and decreased considerably with
increasing PEG content. The slight shear-thinning behav-ior could be observed in unplasticized and plasticized L-
PLA in whole the shear region. The calculated parameters
from the measured rheological properties are summarized
in Table 3. All parameters were obtained by fitting the
modified Cross model as follows [23]:
Z Z0
1 t0gm
; (2)
where Z0 represents the zero shear rate viscosity (Pa s), t0represents the characteristic relaxation time (s), and m
characterizes the slope of the line over the pseudoplastic
region in the logarithmic plot.The Modified Cross model fits the data well. All the
equations have correlation coefficient (r2
) close to 0.95.
As shown in Table 3, the incorporation of PEG led to the
decreasing value of m and decreasing in s0. This referred
that adding more PEG content into L-PLA could lead to
decreasing in relaxation time and slight shear thinning
tendency. This was attributed to the addition of PEG was
easier to cover with PLA chains and the chain of PLA
was disentangled under higher shear rate. Moreover, PLA
blending with PEG also improved the elastomeric behav-
ior of matrix, which would resist the flow and make the
value of m tend to decrease.
As shown in Table 3, g0 decreased significantly with
increasing PEG content and the saturated points of PEG
content seem to be reached resulting in phase separation
[24]. This effect was observed in the PEG concentration
at 15 wt% and 20 wt%. According to theory [25], this
reduction in viscosity can be interpreted as an enhanced
mobility of polymer chain in the system.
CONCLUSIONS
This article demonstrated that plasticizing L-PLA with
PEG could produce a more flexible material with different
mechanical and rheological properties. It was found that
PLA/PEG blends lowered the glass transition temperature
and modified the crystallization properties. It clearly
appeared that the blends obtain a miscibility of the com-
ponents at 5 wt% and 10 wt% PEG content. Mechanical
characteristics of these materials showed a decrease in
modulus and stress at break, but an increase in % elonga-tion at break and impact strength. Nevertheless, L-PLA
blended with PEG became very brittle at higher plasti-
cizer content due to phase separation of PEG phase as
evidence from SEM micrographs.
Rheological study concluded that both unplasticized
and plasticized L-PLA exhibited a slightly shear thinning
behavior at all frequency regions. Viscosities of blends
decreased as PEG content was increased due to increasing
in chain mobility in the system. Moreover, during proc-
essing in the presence of plasticizers with ester groups
could also be potential trans-esterification reactions lead-
ing to a decrease of PLA molecular weights. The moduli
of PLA/PEG blends decreased with increasing plasticizerloading at all frequencies.
At low frequency region, the storage modulus exhib-
ited weak frequency dependence with increasing PEG
content. On the other hand, loss modulus decreased
monotonically with increasing plasticizer loading at all
frequencies.
In this article, plasticizing PEG with linear PLA just
have ability to improve the impact strength. Therefore
with this study we indicate a point of attention for plasti-
cizing branched PLA. A study probing the effect of PEG
on the properties of branched PLA is already in progress.
REFERENCES
1. O. Martin and L. Averous, Polymer, 42, 6209 (2001).
2. D.E. Henton, P. Gruber, J. Lunt, and J. Randall, Natural
Fibers, Biopolymers and Biocomposites, CRC Press, Boca
Raton, FL (2005).
3. K.S. Anderson, S.H. Lim, and M.A. Hillmyer, J. Appl.
Polym. Sci., 89, 3757 (2003).
4. A.M. Gajria, V. Dave, R.A. Gross, and S.P. McCarthy,
Polymer, 37, 437 (1996).
TABLE 3. Rheology characterization of L-PLA and plasticized PLA
melts.
Sample
0 wt%
PEG
5 wt%
PEG
10 wt%
PEG
15 wt%
PEG
20wt%
PEG
g0 868.8 394.7 307.2 186.1 139.1
s0 0.12 0.10 0.09 0.03 0.01
m 0.11 0.15 0.11 0.07 0.09
r2 0.968 0.945 0.983 0.984 0.965
FIG. 10. Dependence of shear viscosity on shear rate at various PEG
concentration of L-PLA/PEG blends at 1808C.
DOI 10.1002/pen POLYMER ENGINEERING AND SCIENCE-2012 115
-
7/30/2019 PES_ornek
9/9
5. M. Sheth, R.A. Kumar, V. Dave, R.A. Gross, and S.P.
McCarthy, J. Appl. Polym. Sci., 66, 1495 (1997).
6. I. Pillin, N. Montrelay, and Y. Grohens, Polymer, 47, 4676
(2006).
7. N. Ljungberg and B. Wesslen, J. Appl. Polym. Sci., 86,
1227 (2002).
8. M.C. Hansen, Prog. Org. Coat., 51, 109 (2004).
9. S. Jacobsen and H.G. Fritz, Polym. Eng. Sci., 39, 1303 (1999).
10. M. Baiardo, G. Frisoni, M. Scandola, M. Rimelen, D. Lips,K. Ruffieux, and E. Wintermantal, J. Appl. Polym. Sci., 90,
1731 (2003).
11. Z. Kulinski and E. Piorkowska, Polymer, 46, 10290 (2005).
12. E.W. Fisher, H.J. Sterzel, and G. Wegner, Colloid. Polym.
Sci., 251, 980 (1973).
13. T. Miyata and T. Masuko, Polymer, 39, 5515 (1998).
14. E. Piorkowska, Z. Kulinski, A. Galeski, and R. Masirek,
Polymer47, 7178 (2006).
15. S.D. Park, M. Todo, K. Arakawa, and M. Koganemaru,
Polymer, 47, 1357 (2005).
16. M. Murariu, A. Silva Ferreira, M. Alexandre, and P. Dubois,
Polym. Adv. Technol., 19, 636 (2008).
17. J. Ferry, Viscoelastic Properties of Polymer, Wiley, New
York (1980).
18. M. Bousmina, P. Bataille, S. Sapieha, and H. Schreiber, J.
Rheol, 39, 499 (1995).
19. Q. Zheng, M. Du, B.B. Yang, and W.G. Polymer, 42, 5473
(2001).
20. M. Du, J. Gong, and Q. Zheng, Polymer, 45, 6725 (2004).21. A. Marcilla and M. Beltran, Handbook of Plasticizers,
ChemTec Publishing Toronto (2004).
22. N. Song, L. Zhu, X. Yan, Y. Xu, and X. Xu, J. Mater. Sci.,
43, 3218 (2008).
23. J.M. Dealy and K.F. Wissbrun, Melt Rheology and Its Role
in Plastics Processing, Van Nostrand Reinhold, New York
(1990).
24. H. Li and M.A. Huneault, Polymer, 48, 6855 (2007).
25. L.A. Utracki, Polymer Alloys and Blends-Thermodynamics
and Rheology, Hanser Publishers, Munich (1990).
116 POLYMER ENGINEERING AND SCIENCE-2012 DOI 10.1002/pen